CN206980733U - Latex maturation reactor - Google Patents
Latex maturation reactor Download PDFInfo
- Publication number
- CN206980733U CN206980733U CN201720936545.2U CN201720936545U CN206980733U CN 206980733 U CN206980733 U CN 206980733U CN 201720936545 U CN201720936545 U CN 201720936545U CN 206980733 U CN206980733 U CN 206980733U
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- latex
- reactor according
- agitating
- maturation reactor
- agitating shaft
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Abstract
Latex maturation reactor is related to latex production field, and in particular to the maturation reactor in a kind of latex production process.Ensure the uniformity stirred during latex maturation, solve the problems, such as the uneven heating of the stirring inequality and natural emulsion brought by tradition stirring.Including reactor body, it is located at intrinsic agitating device and water tank and suction pump below body, the agitating device, which includes mixer and some be located within the body, includes the agitating shaft being located within the body and the motor positioned at agitating shaft top dividing to plate, the mixer on wall.It is heated evenly latex, maturation is successful, improves the qualification rate of final products.
Description
Technical field
It the utility model is related to latex production field, and in particular to the maturation reactor in a kind of latex production process.
Background technology
Turbulent flow is a kind of flow regime of fluid.When flow velocity very little, fluid layering flowing, do not mix mutually, referred to as laminar flow,
Also referred to as current stabilization or piece stream.When flow velocity increases to it is very big when, streamline is no longer clearly apparent, the small whirlpool in many of flow field, laminar flow
Destroyed, adjacent flow interlayer not only has slip, also mixes.At this moment fluid makees irregular movement, has perpendicular to flow tube axis
The component velocity in direction produces, and this motion is referred to as turbulent flow, also known as sinuous flow, flow-disturbing or turbulent flow.
Latex production process needs to carry out maturation, and maturation is an essential important step of foaming process, and maturation is not
Success, causes the unqualified of final products, therefore agitating paddle just plays a significant role.Traditional stirring is exactly that latex is stirring
Mix and rotated under the drive of oar along same direction, laminar flow this aspect can only be rested on, liquid can not be sufficiently stirred, reached
To purpose that is well mixed and being heated evenly.How to be stirred in latex production process and form turbulent flow, so as to improve final products
Qualification rate into urgent problem to be solved.
Utility model content
The utility model is directed to problem above, there is provided a kind of uniformity for ensureing to stir during latex maturation, solves
Because of the latex maturation reactor for the uneven uneven heating problem with natural emulsion of stirring that tradition stirring is brought.
The technical solution of the utility model is：Including reactor body, it is located at intrinsic agitating device and positioned at this
Water tank and suction pump below body, the agitating device include mixer and it is some be located within the body on wall point to plate, it is described
Mixer includes the agitating shaft being located within the body and the motor positioned at agitating shaft top.
If the agitating shaft is provided with dried layer agitating paddle, every layer of agitating paddle is staggeredly placed.
Every layer of agitating paddle includes two blades being located on the same line, the axis folder of each blade and agitating shaft
Angle is 40 ~ 50 °.
The blade is in bending type.
Described point placed longitudinally to plate.
The body is bilayer, forms chuck, and the chuck bottom is provided with water inlet pipe, and chuck top is provided with outlet pipe, institute
State water inlet pipe and outlet pipe is connected with water tank respectively.
Also include integrated circuit case, be provided with heating rod in the water tank, the heating rod is connected with integrated circuit case.
Also include temperature element.
The beneficial effects of the utility model are：Some faults, which put off the agitating paddle put, can ensure latex vertical and horizontal all
It can be stirred to, the agitating paddle of bending type can drive more latexes to flow, and improve stirring capacity；Breast can be upset by dividing to plate
The principle flow direction of glue so that whole flow direction embodies the state rolled from centre to surrounding, good so as to reach
Mixing effect, and then latex is heated evenly, maturation is successful, improves the qualification rate of final products.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model,
Fig. 2 is the utility model decomposing schematic representation,
Fig. 3 is the structural scheme of mechanism of agitating device in the utility model；
1 is body in figure, and 2 be water tank, and 3 be suction pump, and 4 be point to plate, and 51 be agitating shaft, and 511 be blade, and 52 be electricity
Machine, 6 be integrated circuit case.
Embodiment
The utility model is illustrated below in conjunction with the accompanying drawings.
As Figure 1-3, the utility model includes reactor body 1, the agitating device being located in body 1 and positioned at this
Water tank 2 and suction pump 3 below body, the agitating device include mixer and some dividing to plate 4 on the inwall of body 1,
The mixer includes the agitating shaft 51 being located within the body and the motor 52 positioned at the top of agitating shaft 51.Described point longitudinal to plate 4
Place.The principle flow direction of latex can be upset to plate 4 by dividing so that whole flow direction embodies is rolled from centre to surrounding
State, so as to reach good mixing effect.
If the agitating shaft 51 is provided with dried layer agitating paddle, every layer of agitating paddle is staggeredly placed.Every layer of agitating paddle includes
The axis angle of two blades 511 being located on the same line, each blade 511 and agitating shaft 51 is 40 ~ 50 °.Purpose is
In order to stir more latexes, stirring capacity is lifted.
The blade 511 is in bending type.As shown in figure 3, the big stress surface of the body of blade 511 is perpendicular to level side
To being provided with the bending part at an acute angle with horizontal direction parallel or with big stress surface at the top of blade body, it is therefore an objective to
More latexes can be driven to flow.
The body 1 is bilayer, forms chuck, and the chuck bottom is provided with water inlet pipe, and chuck top is provided with outlet pipe, institute
Water inlet pipe and outlet pipe is stated to be connected with water tank 2 respectively.Also include integrated circuit case 6, heating rod is provided with the water tank 2, it is described
Heating rod is connected with integrated circuit case 6.Start heating rod by integrated circuit case 6 to heat the water in water tank 2, heat
Hot water by suction pump 3 from water inlet pipe enter chuck in, intrinsic latex is heated, the water in chuck is from chuck
The outlet pipe in portion is returned in water tank 2, is recycled, saving water resource.
The utility model also includes temperature element.Such as thermometer, temperature sensor, accurately measure latex in reactor
Temperature.
The utility model can make latex in reactor form turbulent flow in stirring, so make latex stir and by
Hot uniformly maturation is successful, improves the qualification rate of final products.
Claims (8)
1. latex maturation reactor, including reactor body, it is located at intrinsic agitating device and the water below body
Case and suction pump, it is characterised in that the agitating device include mixer and it is some be located within the body on wall point to plate, it is described
Mixer includes the agitating shaft being located within the body and the motor positioned at agitating shaft top.
2. latex maturation reactor according to claim 1, it is characterised in that if the agitating shaft stirs provided with dried layer
Oar, every layer of agitating paddle are staggeredly placed.
3. latex maturation reactor according to claim 2, it is characterised in that every layer of agitating paddle is located at including two
Blade on same straight line, the axis angle of each blade and agitating shaft is 40 ~ 50 °.
4. latex maturation reactor according to claim 3, it is characterised in that the blade is in bending type.
5. latex maturation reactor according to claim 1, it is characterised in that described point placed longitudinally to plate.
6. latex maturation reactor according to claim 1, it is characterised in that the body is bilayer, forms chuck, institute
State chuck bottom and be provided with water inlet pipe, chuck top is provided with outlet pipe, and the water inlet pipe and outlet pipe are connected with water tank respectively.
7. latex maturation reactor according to claim 1, it is characterised in that also including integrated circuit case, the water tank
Interior to be provided with heating rod, the heating rod is connected with integrated circuit case.
8. latex maturation reactor according to claim 1, it is characterised in that also including temperature element.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720936545.2U CN206980733U (en) | 2017-07-31 | 2017-07-31 | Latex maturation reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720936545.2U CN206980733U (en) | 2017-07-31 | 2017-07-31 | Latex maturation reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206980733U true CN206980733U (en) | 2018-02-09 |
Family
ID=61417366
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720936545.2U Active CN206980733U (en) | 2017-07-31 | 2017-07-31 | Latex maturation reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206980733U (en) |
-
2017
- 2017-07-31 CN CN201720936545.2U patent/CN206980733U/en active Active
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| GR01 | Patent grant |